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考察了氮气预处理温度对硫代硫酸铵预硫化的Mo/Al2O3催化剂噻吩加氢脱硫(HDS)活性的影响. 采用X射线衍射、高分辨电镜、光电子能谱、热重质谱和硫分析等方法对催化剂进行了表征. 结果表明,预硫化催化剂经80 ℃低温处理并于200 ℃氢气原位活化后噻吩转化率达到最高. 对于氮气低温预处理或常温干燥的预硫化催化剂,载体氧化铝被硫酸根修饰,减少了Mo与载体的相互作用,使得催化剂活化后硫化程度高, MoS2活性相呈多层的Ⅱ型结构,因而HDS活性高. 高于200 ℃的氮气热处理造成硫代硫酸铵的分解,并有少量的多层MoS2活性相生成,但高温热处理造成硫的流失使得活性金属活化后硫化程度偏低,而且MoS2活性相呈现单层的Ⅰ型结构,因而HDS活性较低.

参考文献

[1] Topsoe H;Clausen B S;Massoth F E;Anderson J R,Boudart M.Hydrotreating Catalysis:Science and Technology[M].Beilin:Springer-Verlag,1996:38.
[2] 丁伯强,王鉴,董群,刘忠恩.加氢催化剂预硫化技术进展[J].石化技术与应用,2005(01):56-60.
[3] Welch J G;Poyner P;Skelly R F .[J].Oil & Gas Journal,1994,92(41):56.
[4] Berrebi G .[P].US 4?530?917,1985.
[5] Dufresne P;Legall B;Berrebi G .[P].US 5?397?756,1995.
[6] 于守智;高晓冬;陈若雷 .[P].CN 1200081C,2005.
[7] 李彦鹏,刘大鹏,刘晓,柴永明,刘晨光.器外预硫化型MoNiP/γ-Al2O3催化剂的二苯并噻吩加氢脱硫活性[J].催化学报,2006(07):624-630.
[8] Yamada S;Qian W H;Ishihare A;Wang G Li L Kabe T .[J].Sekiyu Gakkaishi-Journal of the Japan Petroleum Institute,2001,44(04):217.
[9] 李彦鹏,刘大鹏,柴永明,刘晨光.器外预硫化型MoNiP/γ-Al2O3催化剂的加氢脱硫性能研究[J].石油炼制与化工,2006(05):15-19.
[10] Murff S R;Carliste E A;Dufresne P;Rabehasaina H .[J].Preprints-American Chemical Society,Division of Petroleum Chemistry,1993,38(01):81.
[11] De Wind M;Heinerman J J L H;Lee S L;Plantenga F L Johnson C C Woodward D C .[J].Oil & Gas Journal,1992,90(08):49.
[12] Blashka S;Bond G;Ward D .[J].Oil & Gas Journal,1998,96(01):36.
[13] 高玉兰,方向晨,王刚,曹凤兰,李崇慧.器外预硫化加氢催化剂的工业放大[J].炼油技术与工程,2005(04):34-35.
[14] 刘畅,祁兴国,马守波,孙树成,赵法军.加氢催化剂器外预硫化技术进展[J].化学工程师,2006(01):33-38.
[15] Berrebi G;Le Gall B .[P].US 5?139?983,1992.
[16] Roumieu R;Boitiaux J P .[P].US 5?153?163,1992.
[17] De Jong J I;Eisenhuth L;Schoonhoven J W F M;Van Hengstum A J .[P].US 5?139?990,1992.
[18] 葛晖,李学宽,王建国,秦张峰,吕占军,杨英.硫代硫酸铵预硫化的MoO3/Al2O3催化剂的活化和加氢脱硫活性[J].催化学报,2008(09):921-927.
[19] Hui Ge;Xuekuan Li;Zhangfeng Qin .Highly active Mo/Al2O3 hydrodesulfurization catalyst presulfided with ammonium thiosulfate[J].Catalysis Communications,2008(15):2578-2582.
[20] La Parola V;Deganello G;Venezia A M .[J].Applied Catalysis A:General,2004,260(02):237.
[21] Parham T G;Merrill R P .[J].Journal of Catalysis,1984,85(02):295.
[22] De Boer M;Van Dillen A J;Koningsberger D C;Geus J W .[J].Japanese Journal of Applied Physics,1993,32(z32-2):460.
[23] Topsoe H;Hinnemann B;Norskov J K;Lauritsen J V Besenbacher F Hansen P L Hytoft G Egeberg R G Knudsen K G .[J].Catalysis Today,2005,107-108:12.
[24] Kouzu M;Uchida K;Kuriki Y;Ikazaki F .Micro-crystalline molybdenum sulfide prepared by mechanical milling as an unsupported model catalyst for the hydrodesulfurization of diesel fuel[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2004(1/2):241-249.
[25] Alonso G;Berhault G;Aguilar A;Collins V Ornelas C Fuentes S Chianelli R R .[J].Journal of Catalysis,2002,208(02):359.
[26] Hensen E J M;De Beer V H J;Van Veen J A R;Van Santen R A .[J].Catalysis Letters,2002,84(1-2):59.
[27] Hinnemann B;Norskov J K;Topsoe H .[J].Journal of Physical Chemistry B,2005,109(06):2245.
[28] SHANG Hong-Yan;LIU Chen-Guang;ZHAO Rui-Yu;WU Ming-Bo;WEI Fei .XPS Characterization of Carbon Nanotube Supported CoMo Hydrodesulfurization Catalysts[J].Chinese Journal of Chemistry,2004(11):1250-1256.
[29] Texier S;Berhault G;Perot G;Diehl F .[J].Applied Catalysis A:General,2005,293:105.
[30] Alstrup I;Chorkendorff I;Candia R;Clausen B S Topsoe H .[J].Journal of Catalysis,1982,77(02):397.
[31] Duan A J;Wan G F;Zhao Zh;Xu Ch M Zheng Y Y Zhang Y Dou T Bao X J Chung K .[J].Catalysis Today,2007,119(1-4):13.
[32] Van der Aalst M J M;De Beer V H J .[J].Journal of Catalysis,1977,49(03):247.
[33] Arnoldy P;van den Heijkant J A M;De Bok G D;Moulijn J A .[J].Journal of Catalysis,1985,92(01):35.
[34] Vissers J P R;Scheffer B;De Beer V H J;Moulijn J A Prins R .[J].Journal of Catalysis,1987,105(02):277.
[35] Payen E;Kasztelan S;Houssenbay S;Szymanski R Grimblot J .[J].Journal of Physical Chemistry,1989,93(17):6501.
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